[0001] The (N-substituted carbamoyloxy) alkyl acrylates, such as 2-(N-methyl carbamoyloxy)
ethyl acrylate, are well known with the generic class disclosed in U.S. 3,479,328
and U.S. 3,674,838. These compounds have been found particularly effective in radiation
curable compositions since they impart desirable properties to the prepared compositions
and to the cured compositions. However, due to their sensitizing effect and toxicity
they must be handled with extreme caution and, as a consequence, these features detract
from their general acceptance and use.
[0002] The novel (N-substituted carbamoyloxy) alkylene-oxyalkyl acrylate esters of this
invention are those defined by the structural formula:

wherein R is an unsubstituted or substituted (i) linear or branched alkyl group having
from 1 to 4 carbon atoms or (ii) aryl, alkaryl or aralkyl group having 6 or 10 ring
carbon atoms or (iii) cycloalkyl group having from 5 to 8 ring carbon atoms, when
x is 1, or (iv) polyvalent alkylene, arylene,alkarylene, aralkylene or cycloalkylene
having carbon atom values defined for (i) to (iii) supra and a valence equal to the
value of x, when x is greater than 1; wherein the substituents on the R group are
not reactive with the isocyanato radical; R' is hydrogen or alkyl having from 1 to
2 carbon atoms; R" is a linear or branched divalent alkylene of 1 to 10 carbon atoms,
preferably 2 to 4 carbon atoms, divalent cycloalkylene of'5 to 12 carbon atoms, preferably
6 to 8 carbon atoms, or divalent arylene of 6 to 10 ring carbon atoms; X is hydrogen,
methyl or cyano; x has a value of from 1 to 4, preferably 1 or 2; and y is an integer
having an average value of from 1 to 20, preferably from 1 to 6 and most preferably
from 1 to 4.
[0003] The novel compounds of this invention are produced, preferably, by a two-step process
that can, if desired, be carried out sequentially in the same reactor. The compounds
have monofunctionality when a monoisocyanate is used in the second step of the reaction
and polyfunction- ality when a polyisocyanate is used. The polyfunctional acrylyl
compounds can be used as crosslinkers in formulated compositions.
[0004] In the first step of the reaction.a hydroxyalkyl acrylate of the general formula:

wherein X and R" are as previously defined, is reacted with a vicinal alkylene oxide
of the general formula:

wherein R' is as previously defined, to produce the adduct.
[0005] Illustrative of suitable hydroxyalkyl acrylates or methacrylates or cyanoacrylates
one can mention hydroxyethyl acrylate, hydroxyethyl methacrylate, hydroxyethyl cyanoacrylate,
hydroxypropyl acrylate, hydroxybutyl acrylate, hydroxybutyl methacrylate, hydroxydecyl
acrylate, hydroxydecyl cyanoacrylate, hydroxycyclohexyl acrylate, hydroxycyclohexyl
methacrylate, hycroxycyclooctyl acrylate, and the like. Those skilled in the art are
fully familiar with this class of compounds and mixtures can be used.
[0006] Illustrative of suitable vicinal alkylene oxides, one can mention ethylene oxide,
propylene oxide, butylene oxide, or mixtures thereof; when mixtures are used they
can be mixed at any proportions desired.
[0007] The reaction between the hydroxyalkyl acrylates and alkylene oxide is preferably
carried out in contact with a catalyst. The Lewis Acids are suitable as catalysts
and illustrative thereof are boron trifluoride etherate, antimony trifluoride, stannic
chloride, zinc chloride, as well as others known to those skilled in the art. The
catalyst is present in a catalytically effective amount; this can be from 0.1 to 1
weight percent, based on the total weight of reactants charged, preferably from 0.2
to 0.5 weight percent, with from 0.25 to 0.35 weight percent most preferred.
[0008] In the reaction from 1 to about 80 moles, or more, preferably from 1 to 24 moles,
of alkylene oxide are reacted per mole of hydroxyalkyl acrylate. The amount used is
that required to give the desired average y value in formula I; as previously indicated
the preferred average y value is from 1 to 6 and the most preferred value is from
1 to 4.
[0009] The reaction can be carried out at atmospheric or superatmospheric pressure; pressure
is not critical though modest pressure is generally used when reacting an alkylene
oxide, as is known in the art. The reaction time will vary dependent upon the particular
reactants, catalysts, temperature, and batch size involved in any particular instance.
[0010] The reaction temperature will vary from about 20°C to about 125°C and is generally
from about 25°C to about 80°C, preferably from about 55°C to 75°C.
[0011] To minimize olefinic bond free radical polymerization an inhibitor such as the monomethyl
ether of hydroquinone may be present at a concentration of from about 0.01 to 1 weight
percent. Any of the other known inhibitors can be used. It has been noted, however,
that the inhibitors will also slow down the alkylene oxide addition reaction; therefore,
when an inhibitor is used it should be employed at the lowest possible concentration.
[0012] In carrying out the first step, the reaction of the alkylene oxide with the hydroxyalkyl
acrylate; one can charge the hydroxyalkyl acrylate and catalyst to a reactor equipped
with stirring, condensing and cooling means and then the temperature of.the contents
is adjusted to the selected temperature. When this charge is at the desired temperature
the alkylene oxide feed is started and cooling is supplied as required to maintain
the desired temperature during the exothermic feed period. After all of the alkylene
oxide has been added, heating is continued for an additional period of time to assure
completion of the reaction. The resulting adduct can be used in this form in the second
step of the reaction, or it can be treated and the semi-refined or refined adduct
can then be used in the second step of the reaction. The alkylene oxide can be reacted
to produce a random, block or capped adduct by the procedures known in the art.
[0013] Any conventional refining procedure can be used when the adduct is desired in a purer
state. Thus, following the additional heating period the residual adduct can be neutralized
with a base or a diatomaceous earth material such as magnesium silicate, stirred,
heated at reduced pressure to remove volatiles, and then filtered to remove solid
residues. Other procedures can be used that are apparent to those skilled in the art.
[0014] In the second step of the reaction the adduct whose preparation was described above
is reacted with an organic isocyanate.. The suitable isocyanates can be mono=,di-,tri-
or tetra-isocyanates and many such compounds are known and are commercially available.
They can be used singly or in admixture and illustrative thereof'one can mention methyl
isocyanate, ethyl isocyanate, chloroethyl isocyanate, chloropropyl isocyanate, chlorohexyl
isocyanate, chlorobutoxypropyl isocyanate, hexyl isocyanate, phenyl isocyanate, the
o-, m-, and p-chlorophenyl isocyanates, benzyl isocyanate, naphthyl isocyanate, o-ethylphenyl
isocyanate, the dichlorophenyl isocyanates, butyl isocyanate, n-propyl isocyanate,
octadecyl isocyanate, 3,5,5-trimethyl-1-isocyanate-3-isocyana- tomethylcyclohexane,
di(2-isocyanatoethyl)-bicyclo(2.2.1) -hept-5-ene-2, 3-di-carboxylate, 2,4-tolylene
diisocyanate, 2,6-tolylene diisocyanate, 4,4'-diphenylmethane diisocyanate, dianisidine
diisocyanate, tolidine diisocyanate, hexamethylene diisocyanate, the m- and p-xylylene
diisocyanate, tetramethylene diisocyanate, dicyclohexyl-4,4'-methane diisocyanate,
cyclohexane-1,4-diisocyanate, 1,5-naphthylene diisocyanate, 4,4'-diisocyanate diphenyl
ether, 2,4,6-triisocyanato toluene, 4,4',4"-triiso- cyanatotriphenyl methane, diphenylene-4,4-diisocyanate,
the polymethylene polyphenylisocyanates, as well as any of the other organic isocyanates
known to the average skilled chemist.
[0015] It is customary to use any of the known urethane- forming reaction catalysts during
the isocyanate reaction with the polyol. These are well known and any of the catalysts
can be used. Illustrative thereof are dibutyltin dilaurate, stannous octoate, triethylenediamine,
triethylamine, the known tin salt catalysts, and the like. They are generally employed
at a concentration of from about 0.1 to 1 weight percent based onthe weight of the
reaction mixture.
[0016] The amount of isocyanate used is an amount to provide sufficient isocyanato equivalents
to react with the reactive hydroxyl equivalents on the adduct. It is customary to
use a slight excess to assure complete reaction. As previously indicated when a monoisocyanate
is employed the novel N-(substituted carbamoyloxy)alkanoyloxyalkyl (or aryl) acrylate
ester of formula I is monofunctional in respect to acrylyl functionality and when
a polyisocyanate is used such formula I ester is polyfunctional in respect to acrylyl
functionality. The term "acrylyl" includes acrylyl, methacrylyl and cyanoacrylyl groups.
[0017] The second step of the reaction is generally carried out by slowly adding the isocyanate
to the adduct obtained in the first step of the reaction at a temperature of from
about 20° to 90°C, preferably from about 25° to 75°C, and most preferably from about
40° to 55°C. During this addition the mixture is stirred; thereafter stirring is continued
at the selected reaction temperature for a short period of time to assure completion
of reaction. The residual product is then vacuum stripped to remove volatiles and,
if necessary filtered to remove any trace quantities of solid particles. The N-(substituted
carbamoyloxy)alkylene oxyalkyl acrylate ester produced corresponding to formula I
can be used per se or in formulated compositions useful as inks, coatings or adhesives.
[0018] . In producing formulated compositions the novel compounds of this invention are
compounded with activators or catalysts, photoinitiators or photosensitizers, pigments
or colorants, solvents, other reactive components, etc. The formulators skilled in
the art of inks, coatings and adhesives are fully familiar with the requirements in
their respective fields and with the components used in such formulations. Such components
can be formulated with the novel compounds of this invention by the known and conventional
procedures and in the accepted concentrations.
[0019] Thus, when cure is to be accomplished by thermal means a conventional free radical
catalyst or activator is used; when the cure is to be achieved by particulate radiation
such as electron beam radiation, an activator is usually not required; when cure is
to be effected by light radiation such as ultraviolet light, a photosensitizer or
photoinitiator, with optionally an activator therefor, is needed to render the process
commercially acceptable. Coating, ink or adhesive compositions can contain up to 100
weight percent, preferably from 25 to 95 weight percent of the novel compounds of
this invention as the reactive component thereof. The specific identities of the other
components referred to in this and the preceding paragraph are well known to those
skilled in the art and require no further elaboration herein to enable such person
to produce the formulations.
[0020] The following examples serve to further illustrate the invention.
Example 1
Step 1 - Production of 2-Hydroxyethyl Acrylate:Propylene Oxide Adduct
[0021] To a 1-liter stainless steel autoclave there was charged 120.8 grams (1 mole) of
2-hydroxyethyl acrylate and 1.4 grams of boron trifluoride etherate catalyst. The
feed of 348 grams (6 moles) of propylene oxide into this charge was begun at a temperature
of 21°C. The reaction was strongly exothermic, requiring efficient cooling. The temperature
was allowed to increase to about 50°C and the feed rate and cooling then adjusted
to maintain a temperature of 55-60°C at a feed rate of about 60 grams per hour over
the remainder of the five- hour feed period. When all the feed was in, the reactor
showed a pressure of 7 x 10
3Pa; this fell to zero after one hour at 60°C. The temperature was then reduced to
50-52°C and a vacuum of 0.26 x 10
3 - 0.40 x 10
3pa (2-3mm Hg) was applied for 0.5 hour to remove volatiles. The stripped product was
treated for 2 hours at 70°C with 6.2 grams of magnesium silicate to neutralize catalyst
residues. After filtration to remove neutralized catalyst residues and magnesium silicate
there was obtained 316 grams of a clear, slightly yellow liquid having an hydroxyl
number of 149.9 and a Brookfield viscosity of 24.2 x 10
-6 m
2/s at 38°C. According tothe chemical end group analysis, the average add-on of propylene
oxide was about 4.4 moles.
Step 2 - Production of (N-Methylcarbamayloxy) polypropyl- eneoxyethyl acrylate
[0022] To a 500 ml amber glass kettle fitted with a stirrer, thermometer and feed tank there
were charged 100 grams (0.27 moles) of the adduct of Step 1 and 0.15 gram of dibutyltin
dilaurate catalyst. Over a period of 30 minutes at a temperature of 45-50°C a total
of 15.7 grams (0.36 mole) of methyl isocyanate was fed in and then the mixture was
heated for four hours at 50°C and then stripped free of volatiles for 1 hour at 45°C
and 2 x 10
3Pa (15 mm Hg) pressure. The product was a very fluid, light yellow material having
a residual isocyanato content of 0.11% by analysis and the average formula:
[0023]

Example 2
Step 1 - Production of 2-Hydroxyethyl Acrylate:Ethylene Oxide Adduct
[0024] To .the same type equipment describedin Step 1 of Example 1 there was charged a mixture
of 241.6 grams (2 moles) of 2-hydroxyethyl acrylate, 2.8 grams of boron trifluoride
etherate, and 0.21 gram of 2,6-di-tertiary butyl-p-cresol. Over a total of 4 hours
there was fed into this charge 352 grams (8 moles) of ethylene oxide at a temperature
maintained at 46-49°C by means of efficient cooling. After stirring another hour at
30°C, the charge was treated with 11.6 grams of magnesium silicate and stripped free
of volatiles at full vacuum while holding the temperature at 70°C for two hours. After
filtration there was obtained 519 grams of clear, water-white liquid having a viscosity
of 28 x 10
-6m
2/s at 38°C and an hydroxyl number of 147.1
Step 2 - Production of (N-Methylcarbamoyloxy)polyethyl- eneoxyethyl acrylate
[0025] In a manner similar to that described in Step 2 of Example 1, 300 grams of the above
adduct and 0.45 gram of dibutyltin dilaurate catalyst were reacted with methyl isocyanate
by feeding into the charge 45 grams of methyl isocyanate over a 20-minute period at
55°C. After a four-hour cookout at 45-49°C, the kettle contents showed no free isocyanate.
A total of 320.5 grams of this product was stripped at 70°C for 1 hour at full vacuum
on a Rotary Evaporator to afford 314 grams of product as a very mobile, light yellow
liquid having a Brookfield viscosity of 63 x 10
-6 m
2js at 38°C and a Gardner color of 1.0 and the average formula:

Example 3
Step 1 - Production of 2-Hydroxyethyl Acrylate:Ethylene Oxide Adduct
[0026] In equipment and manner similar to that described in Step 1 of Example 1,471.1 grams
(3.9 moles) of hydroxyethyl acrylate, 4.2 grams boron trifluoride etherate and 0.32
gram of 2.6-di-tertiary butyl-p-cresol were reacted with 343.2 grams (7.8 moles) of
ethylene oxide. There was obtained, after neutralization with 16 grams of magnesium
silicate for 1.5 hours at 90°C, stripping at 90°C for 0.5 hour at full vacuum and
filtration, 700 grams of clear, almost white liquid exhibiting an hydroxyl number
of 218, which calculates to a molecular weight of 259. The product color was 1.0 Gardner
and the Brookfield viscosity was 18.2 x 10
-6 m
2/s at 38°C. The adduct produced contained an average of two ethyleneoxy units.
Step 2 - Production of (N-Methylcarbamoyloxy)polyethyl- eneoxyethyl acrylate
[0027] In a manner similar to that described in Step 2 of Example 1, the above adduct was
reacted with monoisocyanate by feeding 66 grams of methyl isocyanate to a mixture
of 300 grams of the adduct and 0.45 gram of dibutyltin dilaurate catalyst. After reaction
and stripping at 70-75°C at 0.:65 x 10
3Pa (5mm Hg) pressure, there was obtained 361 grams of a liquid product having a Gardner
color of 1, a Brookfield viscosity of 36.6 x 10
-6 m
2/s at 38°C.and a free isocyanato content of 0.01%.
[0028] In a similar manner the adduct of Step 1 is reacted with tolylene diisocyanate or
hexamethylene diisocyanate to produce the corresponding diacrylate compounds.
Example 4
Step 1 - Production of 2-Hydroxyethyl Acrylate:Ethylene Oxide Adduct
[0029] In a manner similar to that described in Step 1 of Example 1, 300 grams (3.9 moles)
of 2-hydroxyethyl acrylate was reacted with 10..7 moles of ethylene oxide in the presence
of 4.2 grams of boron trifluoride etherate and 0.32 gram of 2,6-di-tertiary butyl-p-cresol.
There was recovered after neutralization, stripping and filtration 830 grams of water-white
liquid adduct having an hydroxyl number of 201, a specific gravity of 1.129 at 25°C
and an average of three ethyleneoxy groups.
[0030] In a similar manner the adduct is produced using 2-hydroxypropyl acrylate or methacrylate
or 4-hydroxycyclohexyl acrylate in place of the 2-hydroxyethyl acrylate.
Step 2 - Production of (N-Methylcarbamoyloxy)polyethylene oxy ethyl acrylate
[0031] In a manner similar to that described in Step 2 of Example 1, 300 grams of the adduct
of Step 1 was reacted at 45-50°C. with 61.3 grams of methyl isocyanate in the presence
of 0.45 grams of dibutyltin dilaurate catalyst. There was obtained 355 grams of stripped
product as an almost colorless liquid having a specific gravity of 1.057 at 20°C,
a Gardner color 1.0, a Brookfield viscosity of 45.6 x 10
-6m
2/s at 38°C and a free isocyanato content of 0.01%; it contained an average of about
three ethyleneoxy units.
Example 5
Step 1 - Production of 2-Hydroxyethyl Acrylate:Propylene Oxide Adduct
[0032] In a manner similar to that described in Step 1 of Example 1, 2 moles of 2-hydroxyethyl
acrylate was reacted with 4 moles of propylene oxide in the presence of 2.8 grams
of boron trifluoride at 45-48°C. There was obtained 444 grams of neutralized, stripped
and filtered liquid product having Gardner 1.0 color, Brookfield viscosity of 11.7
x 10
-6m
2/s at 38°C and an average of two propyleneoxy units.
[0033] In a similar manner the adduct is produced using a mixture of ethylene oxide and
propylene oxide.
Step Production of (N-Methylcarbamoyloxy)polypropy- leneoxyethyl acrylate
[0034] In a manner similar to that described in Step 2 of Example 1, 244 grams of the adduct
of Step 1 was reacted with 62.6 ml. of methyl isocyanate at 45-50
0C using 0.35 gram of dibutyltin dilaurate catalyst. After a four hour reaction at
45-50°C and a one hour vacuum stripping (0.65 x 10
3Pa or 5mmHg) at 50°C, 297 grams of liquid, capped product was obtained with a specific
gravity of 1.099 at 25°C, a color of 1 Gardner, a Brookfield viscosity of 34.1 x 10
-6m
2/s at 38°C, a free isocyanato content of 0.01% and an average of about two propyleneoxy
units.
Example 6
Step 1 - Production of 2-Hydroxyethyl Acrylate:Propylen Oxide Adduct
[0035] In a manner similar to that described in Step 1 of Example 1, an adduct was prepared
by feeding 8 moles of propylene oxide to a mixture of 2 moles of hydroxyethyl acrylate
in the presence of 2.8 grams of boron trifluoride etherate. The feed time required
was one hour at 44-48°C. The recovery of neutralized, stripped product was 638 grams;
it had a Gardner color of 1, a Brookfield viscosity,of 17.4 x 10
-6 m
2/s at 38°C and an average of about four propyleneoxy units.
Step 2 - Product of (N-Methylcarbamoyloxy)polypropylene- oxyethyl acrylate
[0036] In a manner similar to that described in Step 2 of Example 1, 300 grams of the adduct
of Step 1 above was reacted with 51.3 ml of methyl isocyanate in the presence of 0.45
gram of dibutyltin dilaurate catalyst at 45-50
cO. The stripped product (341 grams) exhibited a specific gravity of 1.074 at 25°C,
a color of 1 Gardner and a Brookfield viscosity of 46.6 x 10
-6 m
2Is at-38°C. The residual free isocyanato content was 0.008%; it had an average of
about 4 propyleneoxy units.
[0037] A series of curable compositions was prepared using the reactive novel (N-alkylcarbamoyloxy)polyalky-
leneoxyalkyl acrylates produced in Examples 3 to 6. The compositions were prepared
by producing an acrylated polyester urethane oligomer in the reactive novel acrylates
produced in Step 2 of the above examples as the solvent medium for the oligomer formation
reaction. The procedure followed was to initially charge 17.3 g of the reactive novel
acrylate of this invention as reactive solvents, 2 drops of dibutyltin dilaurate catalyst
and 14.7 g of isophorone diisocyanate to a.reactor and then heat the mixture to 50°C.
To this mixture there was slowly added 17.6 g of polycaprolactone diol having an average
molecular weight of 530 followed by the slow addition of 8 g of 2-hydroxyethyl acrylate;
the temperature was maintained at about 50°C. After all of the reactants had been
added, the mixture was stirred to assure completion of the reaction (Runs 1 to 4).
For comparative purposes a similar composition was produced by the same process .using
17.3 g of 2-ethylhexyl acrylate (2-EHA) as the reactive solvent (Run 5). To each composition
there was also added 0.01 g of monomethyl ether of hydroquinone as inhibitor and 0.6
g of di-sec-butoxyacetophenone as photoinitiator.
[0038] The liquid compositions were applied to steel panels and cured by exposure to ultraviolet
light radiation in a nitrogen atmosphere. The dry, cured films were removed from the
panels and evaluated. The data revealed that the compositions containing the reactive
novel acrylates of this invention produced'films having significantly superior tensile'properties
than film obtained using the commercial reactive monomer solvent employed in Run 5.
Further, the reactive novel acrylates of this invention are less volatile, cure more
rapidly and exhibit less odor, all significant economic and environmental considerations.
The results of this series are reported in the following table; tensile and elongation
were measured using ASTM-D-638.
